CN203095822U - High sludge dewatering drying device - Google Patents
High sludge dewatering drying device Download PDFInfo
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- CN203095822U CN203095822U CN201320021452.9U CN201320021452U CN203095822U CN 203095822 U CN203095822 U CN 203095822U CN 201320021452 U CN201320021452 U CN 201320021452U CN 203095822 U CN203095822 U CN 203095822U
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- 239000010802 sludge Substances 0.000 title claims abstract description 40
- 238000001035 drying Methods 0.000 title claims abstract description 15
- 238000005192 partition Methods 0.000 claims abstract description 24
- 239000004744 fabric Substances 0.000 claims abstract description 16
- 238000001125 extrusion Methods 0.000 claims abstract 6
- 230000014759 maintenance of location Effects 0.000 claims description 10
- 230000018044 dehydration Effects 0.000 claims description 7
- 238000006297 dehydration reaction Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000009933 burial Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
Description
技术领域 technical field
本实用新型专利涉及一种污泥高度脱水,尤其涉及一种污泥高度脱水的干化装置。 The utility model patent relates to a highly dehydrated sludge, in particular to a drying device for highly dehydrated sludge.
背景技术 Background technique
传统的板框压滤机,过滤时单靠进泥泵的压力在板框间滤室内形成泥饼,由于不具备再次处理的功能,导致处理后泥饼含水率高达(85%~90%),不能达到深埋或焚烧的要求,还需进行二次处理。目前市场上在销售的改进型隔膜压滤机,虽然在传统压滤机上增加了再次压滤工艺,由于隔膜材料和工艺的限制,存在以下缺点: The traditional plate and frame filter press only relies on the pressure of the mud inlet pump to form mud cake in the filter chamber between the plate and frame during filtration. Since it does not have the function of reprocessing, the moisture content of the mud cake after treatment is as high as 85% to 90%. , cannot meet the requirements of deep burial or incineration, and secondary treatment is required. The improved diaphragm filter press currently on the market has the following disadvantages due to the limitations of the diaphragm material and process, although the re-press filtration process has been added to the traditional filter press:
1、一是再次压滤的压力不能太高, 1. First, the pressure of the filter press should not be too high.
2、二是由于隔膜技术的膨胀系数小所以压缩空间有限, 2. Second, due to the small expansion coefficient of the diaphragm technology, the compression space is limited.
3、三是由于隔膜空间固定,再次压滤时的高压只能局部施加在滤室的泥饼上, 3. The third is that due to the fixed space of the diaphragm, the high pressure during the second filter press can only be partially applied to the mud cake in the filter chamber.
4、四是由于以上的缺陷和不足,若再次压滤时滤室内形成的泥饼含水率高(95%~90%),则再次压榨的作用不大, 4. Fourth, due to the above defects and deficiencies, if the mud cake formed in the filter chamber has a high moisture content (95% to 90%) during the second press, the effect of the second press is not great.
所以目前市场在销售的压滤机产品中,由于受到本身技术和工艺的限制,还有水质、污泥特性等条件的不同,隔膜压滤机再次压榨后也只能在将原来滤室内的泥饼含固率提高一倍(理想状态含水率70%左右),不能完全满足客户的需求。 Therefore, among the filter press products sold in the market at present, due to the limitation of its own technology and process, as well as the different conditions such as water quality and sludge characteristics, the diaphragm filter press can only re-press the mud in the original filter chamber. Double the solid content of the cake (the ideal moisture content is about 70%), which cannot fully meet the needs of customers.
实用新型内容 Utility model content
本实用新型主要是解决现有技术中存在的不足,提供一种经济、简便的污泥脱水工艺技术,一次性污泥脱水至含水率50%以下的污泥高度脱水的干化装置。 The utility model mainly solves the deficiencies in the prior art, and provides an economical and convenient sludge dehydration process technology, a one-time sludge dehydration device for highly dewatered sludge with a moisture content below 50%.
本实用新型的上述技术问题主要是通过下述技术方案得以解决的: The above-mentioned technical problems of the utility model are mainly solved by the following technical solutions:
一种污泥高度脱水的干化装置,包括固定推架和移动推架,所述的固定推架与移动推架间设有呈均匀连续状分布的过滤隔板,所述的过滤隔板间设有高压滤板,所述的高压滤板中设有呈连通状分布的挤压软管,所述的挤压软管的两侧分别设有与高压滤板相固定的滤布层,所述的挤压软管的一端呈封闭状,所述的挤压软管的另一端延伸出高压滤板,所述的固定推架、过滤隔板和高压滤板中分别设有与之相连通的污泥进料孔。 A drying device for high degree of sludge dehydration, comprising a fixed push frame and a movable push frame, between the fixed push frame and the movable push frame are provided with evenly and continuously distributed filter partitions, between the filter partitions A high-pressure filter plate is provided, and the high-pressure filter plate is provided with extruded hoses distributed in a connected shape. The two sides of the extruded hoses are respectively provided with filter cloth layers fixed to the high-pressure filter plate. One end of the extruded hose is closed, and the other end of the extruded hose extends out of the high-pressure filter plate, and the fixed push frame, the filter partition and the high-pressure filter plate are respectively equipped with sludge feed hole.
作为优选,所述的过滤隔板的两侧端分别设有内凹状的污泥置留槽,所述的污泥置留槽的横截面呈梯形状,所述的滤布层与挤压软管相贴合分布,所述的滤布层与高压滤板间设有污泥扩充槽,所述的挤压软管的直径为25~65mm。 As a preference, concave sludge retention tanks are respectively provided on both sides of the filter partition, the cross-section of the sludge retention tank is trapezoidal, and the filter cloth layer and the extruded soft The pipes are arranged in close contact with each other, and a sludge expansion tank is arranged between the filter cloth layer and the high-pressure filter plate, and the diameter of the extruded hose is 25-65 mm.
作为优选,所述的挤压软管与进压管相连通。 Preferably, the extruded hose is in communication with the pressure inlet pipe.
本实用新型主要特点及优点: Main features and advantages of the utility model:
本实用新型采用的高压软管能耐压3.0MPa,能用较高压力进行再次压榨,这是目前隔膜压滤机难以做到的,所以压滤后的泥饼能过到含水率50%以下。采用的高压软管可以根椐不同客户水质及污泥的特性及需求,采用不同的压力进行再次压榨(1.5MPa~2.5MPa),做到经济高效,高压软管平铺在滤室仓内,由于软管的膨胀系数为4~9倍,没有空间限制,软管内的高压能全部均匀的作用在滤室内的泥饼上,达到高压压榨的目的而取得更高的含固率。采用的高压软管膨胀系数大,膨胀后的体积大于滤室容积,滤室内泥饼含水率高低都能一次性压榨到客户需求的设计要求(含水率50%)。 The high-pressure hose used in the utility model can withstand pressure of 3.0MPa, and can be squeezed again with a higher pressure, which is difficult for the current diaphragm filter press, so the mud cake after pressing can pass to a water content below 50%. . The high-pressure hose used can be re-pressed with different pressures (1.5MPa~2.5MPa) according to the characteristics and needs of different customers' water quality and sludge, so as to achieve economical efficiency. The high-pressure hose is laid flat in the filter chamber. Since the expansion coefficient of the hose is 4 to 9 times, there is no space limitation, and the high pressure in the hose can all act on the mud cake in the filter chamber evenly, achieving the purpose of high pressure pressing and obtaining a higher solid content. The high-pressure hose used has a large expansion coefficient, and the volume after expansion is larger than the volume of the filter chamber. The moisture content of the mud cake in the filter chamber can be squeezed to meet the design requirements of the customer (moisture content 50%) at one time.
因此,本实用新型的污泥高度脱水的干化装置,结构紧凑,干化步骤简洁高效。 Therefore, the highly dewatered sludge drying device of the present utility model has a compact structure, and the drying steps are simple and efficient.
附图说明 Description of drawings
图1是本实用新型的结构示意图; Fig. 1 is a structural representation of the utility model;
图2是图1中高压滤板的结构示意图。 Fig. 2 is a schematic structural view of the high-pressure filter plate in Fig. 1 .
具体实施方式 Detailed ways
下面通过实施例,并结合附图,对本实用新型的技术方案作进一步具体的说明。 The technical solutions of the present utility model will be further specifically described below through the embodiments and in conjunction with the accompanying drawings.
实施例1:如图1和图2所示,一种污泥高度脱水的干化装置,包括固定推架1和移动推架2,所述的固定推架1与移动推架2间设有呈均匀连续状分布的过滤隔板3,所述的过滤隔板3间设有高压滤板4,所述的高压滤板4中设有呈连通状分布的挤压软管5,所述的挤压软管5的两侧分别设有与高压滤板4相固定的滤布层6,所述的挤压软管5的一端呈封闭状,所述的挤压软管5的另一端延伸出高压滤板4,所述的固定推架1、过滤隔板3和高压滤板4中分别设有与之相连通的污泥进料孔7。
Embodiment 1: As shown in Figure 1 and Figure 2, a drying device for highly dewatered sludge comprises a fixed push frame 1 and a
所述的过滤隔板3的两侧端分别设有内凹状的污泥置留槽8,所述的污泥置留槽8的横截面呈梯形状,所述的滤布层6与挤压软管5相贴合分布,所述的滤布层6与高压滤板4间设有污泥扩充槽10,所述的挤压软管5的直径为25mm。所述的挤压软管5与进压管9相连通。
Both sides of the
实施例2:一种污泥高度脱水的干化装置,其特征在于:包括固定推架1和移动推架2,所述的固定推架1与移动推架2间设有呈均匀连续状分布的过滤隔板3,所述的过滤隔板3间设有高压滤板4,所述的高压滤板4中设有呈连通状分布的挤压软管5,所述的挤压软管5的两侧分别设有与高压滤板4相固定的滤布层6,所述的挤压软管5的一端呈封闭状,所述的挤压软管5的另一端延伸出高压滤板4,所述的固定推架1、过滤隔板3和高压滤板4中分别设有与之相连通的污泥进料孔7。
Embodiment 2: A drying device for high degree of sludge dehydration, characterized in that: it includes a fixed push frame 1 and a
所述的过滤隔板3的两侧端分别设有内凹状的污泥置留槽8,所述的污泥置留槽8的横截面呈梯形状,所述的滤布层6与挤压软管5相贴合分布,所述的滤布层6与高压滤板4间设有污泥扩充槽10,所述的挤压软管5的直径为40mm。所述的挤压软管5与进压管9相连通。
Both sides of the
实施例3:一种污泥高度脱水的干化装置,其特征在于:包括固定推架1和移动推架2,所述的固定推架1与移动推架2间设有呈均匀连续状分布的过滤隔板3,所述的过滤隔板3间设有高压滤板4,所述的高压滤板4中设有呈连通状分布的挤压软管5,所述的挤压软管5的两侧分别设有与高压滤板4相固定的滤布层6,所述的挤压软管5的一端呈封闭状,所述的挤压软管5的另一端延伸出高压滤板4,所述的固定推架1、过滤隔板3和高压滤板4中分别设有与之相连通的污泥进料孔7。
Embodiment 3: A drying device for high degree of sludge dehydration, characterized in that: it includes a fixed push frame 1 and a
所述的过滤隔板3的两侧端分别设有内凹状的污泥置留槽8,所述的污泥置留槽8的横截面呈梯形状,所述的滤布层6与挤压软管5相贴合分布,所述的滤布层6与高压滤板4间设有污泥扩充槽10,所述的挤压软管5的直径为65mm。所述的挤压软管5与进压管9相连通。
Both sides of the
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| CN201320021452.9U CN203095822U (en) | 2013-01-16 | 2013-01-16 | High sludge dewatering drying device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103113011A (en) * | 2013-01-16 | 2013-05-22 | 俞一鸣 | Desiccation device and method of sludge through high dehydration |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103113011A (en) * | 2013-01-16 | 2013-05-22 | 俞一鸣 | Desiccation device and method of sludge through high dehydration |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130731 Termination date: 20160116 |
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| EXPY | Termination of patent right or utility model |